A detailed experimental study is carried out to investigate the flow struct
ure and heat transfer in a converging horizontal channel with localized hea
ting on the bottom surface. This configuration arises in typical chemical v
apor deposition (CVD) systems and the impact of the transport mechanisms on
the deposition process is of particular interest. Experimental observation
s of various flow circumstances indicate the appearance of longitudinal and
transverse roll structures. These flow structures have direct implications
with respect to CVD processing where deposition rates and film quality are
critically dependent on reactive species and byproduct transport onto the
deposition surface. Different flow regimes are observed for typical operati
ng conditions, and their existence is described using regime maps. Regime b
oundaries are correlated in terms of important parameters that describe the
flow rate, heating rate, and tilt angle. A regime transition from longitud
inal rolls to transverse rolls occurs at around Gr/Re-2 = 6000, while the c
ritical Rayleigh number is found to be dependent on the flow. Heat transfer
correlations are also derived and it is seen that the heating rate is the
dominant effect on the susceptor temperature, while the effects of flow rat
e and tilt angle are small. The implication of heat transfer results on mas
s transfer are discussed for horizontal CVD reactors. The flow structure an
d heat transfer phenomena observed in this study yield valuable insight int
o the basic buoyancy and forced-flow-induced transport in horizontal channe
ls as well as guidelines for the modeling and design of CVD systems. (C) 20
00 American Institute of Physics. [S1070-6631(00)01907-3].